Process for making butadiene



y 1946- I. L. ,MURRAY ET AL 2,403,742

PROCESS FOR MAKING BUTADIENE Filed Sept. 9, 1943 g0 g HYDROGEN A T L T 1 BUT DIENE Q -9 55 a A T m E Q Q 5: 2' E E INVENTORS Fri-152m. I lRVlN L. MURRAY 75 1* $6145 2 QFAI FH JR 55f g 1 BY y ATTORNEY Patented July 9, 1946 PROCESS FOR -MAKIN G ,BUTADIENE Irvin L. .Murray, Charleston, and Jay L. Marsh, South Charleston, W. Va., and Silas P. Smith, JL, Louisville, Ky, assignors to Carbide and Carbon Chemicals Corporation, a corporation of New York I Application-September 9, 1943, Serial No. 501,611

This invention relates to a process for making butadiene from ethanol.

According to this invention, butadiene is formed from ethanol in twosteps, one step being the conversionof ethanol to acetaldehydein a separate reaction, and the other step beingthe separateconversibn to butadiene of a mixture of theacetaldehyde formedin' the first stepi and ethanol. Both reactions are carried out inthe vaporphase, Although; some savingsin the total heat required to operate both. steps, of the'process may'be obtained by introducingthe-gaseous re action products-from the i acetaldehyde converter directly into the butadiene converter, greater advantages. in economyw-and ease of operation are obtained bythe process of thisinvention. In this invention, the products from both the; acetalde hyde and the butadiene converters arezseparated from permanent gasesproducedin, the reactions, the butadiene is separated from any unreacted ethanol and acetaldehyde, and the materials remaining from these separations, containing eth anol, acetaldehyde and by-products areintroduced to a common distillation system. This distillation system removes the by-products producedin both reactions and supplies ethanol to the acetaldehyde' converten; and ethanol and acetalde'hydeto the *butadiene converters Thus, the entire process is Operated-i113 cyclicand continuous; manner. EthanoLequivalent to that consumed in the process, is. supplied to the system,.

preferably'as reflux'in a distillation column in which ethanol vaporsare beingremoved. However, make-up ethanol may be supplied in "any other convenient manner. ,For instancait'may beadded as scrubbing liquid to separate butadiene from. other gases of lower boiling point.

The process of" this invention has theadvantae'e that, by providing appropriate storage facilities for the crude productsof eachreaction; each reaction may be conducted independently. IA further advantageis that'iboth reaction systems utilize the same distillation system for the recovery ofhnconverted materials, which provides econmay in "the equipmentrequ-ired to operate the process. Inthe first stepgof the process, ethanol vapors are passed toa reaction; zone, and a part of such vapors'convertedxto acetaldehyde by any of the known methods. I drogenation of the ethanolto acetaldehyde in the presence of dehydrogenation catalysts, or the catalytic oxidation of ethanol, toacetaldehyde-by molecular oxygen; Theproducts from .this reac- These, methods include dehy- 8' Claims. (omen-cs1) vtion containing ac'etaldehydeandyethanol are 55;

condensed. Any permanent gases produced'in the reaction, .or present in the reaction products, also contain the vapors of this condensate, namely, acetaldehyde, ethanol, Water and byproducts. The valuable constituents may be recovered fromjthese gases by compressing .the

, gases andscrubbing them with water.

In the second step of the process, ethanol and acetaldehyde, preferably in 'the'molar' ratio of about 3 to 1, are reacted 'in the' vapor tate in the presence of suitablej .catalystsf to form butadiene. A preferred catalystis described in W. J. Tonssaint and J. 'I'. Dunn application Serial No. $60,120, filed September 29, 1942. Other catalysts for this reaction are, reported in the literature. Theiefiluentvapors and gases. from the butadie'ne converter, containing butadiene, ethanol, acet aldehyde, diethyl'ether, ethylene, propylene and saturated hydrocarbon gases, and other by-p'ro'd nets are. passed through a condenser. Most of the vapors are condensed in this operation, but

alargeffraction of the butadiene is notliquefied and suchjfract'ion is presentin the gases. leaving the condenser. ,The butadiene' may be recovered from. such gases by compressing the gases and scrubbingthem' with a solvent, such as ethanol. Howeveneconomyin operation maybe obtained by employing. as the scrubbing liquid a material which is to be'subjected to distillation 'inany event as described in the copending application, Process' for making butadiene, Serial No. 501,610, of I, L., Murray, J. L. Marsh and S. P. :Smith,;Jr. Such a material is the condensate of ethanoland acetaldehyde from the acetaldehyde reaction. Alternatively, the make-up ethanol required in the process-may be employed as scrubhing. liquid.

.Asubsequentscruhbing tower may be provided tore'cover thevapors of the scrubbing liquid: from thelgasesleavingthe butadiene scrubbing tower. Watefisasuitabl'e scrubbing liquid for use in this second tower.

The first condensate from the butadiene reaction and the liquid. efilux from the scrubbing'tower win whichibutadieneis removed from other gases maybe purified, if necessary, by known methods.

The condensatesstill residuesand liquid scrubber products from the previousv operations which contain all the effluent materials" ofboth reaction system with the exception of butadiene, hydrocarbon impurities associated with the butadiene, and the permanent gases, are subjected to a series of distillations. The streams remaining after the separation of butadiene and other gases contain ethanol, acetaldehyde, water, and by-products, such as diethyl ether, which i formed in the butadiene reaction, and miscellaneous byroducts of the acetaldehyde-forming reaction, such as ethy1 acetate, acetic acid and butyraldehyde. The distillation system removes sufficient of the by-products to prevent thei accumulation in the verter need not be operated at undesirably high pressures in order to compensate for the pressure drop through both converters. If such high pressures were maintained, the yield of acetaldehyde by the dehydrogenation of ethanol would be decreased. The alternative to this, in which compressors are provided between the acetaldehyde converter and the butadiene converter, would cyclic system, and recovers ethanol and acetaldehyde for passage to the acetaldehyde and butadiene reaction systems. One method by which this may be accomplished is to provide a series of stills adapted to remove the components in the order of their volatility. The first column in such a series removes acetaldehyde from the feed for passage to the butadiene converter. The acetaldehyde distills as its azeotropic mixture with diethyl ether, boiling at about 57 C. at 40 p. sci. gauge pressure and containing approximately 75% acetaldehyde and diethyl ether. Relatively large amounts of diethyl ether thus accumulate in the cyclic system and are recirculated through the butadiene converter. Thi tends to prevent the formation of additional amounts of diethyl ether in the reaction.

The residue from this distillation passes to another continuous column where the lay-products are removed as a heads product containing a mixture of binary and ternary azeotropes involving acetaldehyde, water, diethyl ether, ethyl acetate, butyraldehyde and otherimpurities. A batch still may be provided for the periodic recovery from the by-prcducts of the materials employed in the process.

The residue from the by-products removal still, consisting largely of ethanol and water, passes to an alcohol still operated under pressure, which generates an azeotropic mixture of ethanol and water for feeding both reaction systems. The

water removed as a residue is customarily used 7 for heating purposes before being discarded. Thus, it may be employed for heating the feed to the still in which acetaldehyde is removed and the feed to the still in which butadiene is removed.

Various methods of removing by-products,

other than as indicated, may also be practiced,

as by withdrawing by-products from plates in the butadiene, acetaldehyde, by-products, and ethiutiol column, in which such by-produ'cts accumu- Other arrangements of the distillation series may be carried out in which the materials to :be separated are divided into two or more fractions, and such fractions treated to isolatethe components, rather than the successive removal of each component in the order of its volatility, as described above.

The process of this invention represents an integrated process for making butadiene from ethanol, in which the acetaldehyde formed by dehydrogenationof ethanol is not passed directly into the butadiene converter, but, instead, is first passed to a recovery distillation system which produces acetaldehyde, largely freed from impurities formed in both reactions, for passage to the butadiene converter, and recovers unreacted ethanol. This process possesses the advantage over a process in which the products from the acetaldehyde converter are fed directly into the butadiene converter, in that the acetaldehyd congreatly increase the cost of the installation and would make operation of the process more complex.

In addition, they passage of the 'by-products from the acetaldehyde reaction, including hydrogen, through the butadiene converter might tend to injure the butadiene catalyst, reduce the yield of butadiene, or form other lay-products troublesome to remove.

Suitable apparatus and operating conditions for practicing the process described abov will now be described with reference to the attached drawing but the invention isnot restricted to these specifi embodiments. All proportions specified are by weight.

Ethanol vapors alOng with about 10% water vapor are introduced to a converter ID of the shell-and-tube type, through a pipe I I, after passing through a heat exchanger 12. The converter contains a copper catalyst at a temperature of about 280 C. and part of the ethanol is dehydrogenated to acetaldehyde in passing over this catalyst. The converter may be heated by circulating a high-boiling organic liquid through heating elements in the converter. The vapors leave the bottom of the converterthrough a' pipe l3, pass through the heat exchanger l2 used to preheat the feed, and pass through a pipe I4 to a condenser |5,in which most of the vapors are condensed.

v The uncondensed vapors, the gases and the condensate pass through a pipe I E to a separating tank IT, in which the condensate collects at the bottom. The uncondensed vapors and gases containing acetaldehyde, ethanol, water and hydrogen pass from the top of the tank through a pipe l8 to a compressor [9, where they are compressed to a pressure of about p. s. i. The compressed vapors and gases pass through a condenser 20, from which they are introduced through a pipe 2| to the base of a scrubbing tower 22. Here, the water-soluble vapors are dissolved'and re- -moved from the hydrogen by means of scrubbing water, and the liquid effluent flows through pipe 23 to the recovery distillation system.

The chemical reaction producing butadiene is conducted concurrently with that producing acetaldehyde In this second chemical reaction, a mixture of ethanol and acetaldehyde vapors, preferably in the molar ratio of about 3 to 1, is passed through a heat exchanger 24 through a pipe 25 to a converter 26. The converter contains a catalyst of an appropriate type at a temperature oi 300 to 350 C. Part of the ethanol and acetaldehyde are converted to butadiene in the converter, and the efliuent vapors pass through a pipe 21 to the heat exchanger 24 which preheats the reactants. The vapors leave the heat exchanger through a pipe 28, and pass to a condenser 29, where more than half of both the butadiene and the acetaldehyde, and almost all the ethanol, are condensed. The vapors and condensate pass through pipe 9 to a settling tank 30, where the condensate is drawn ofi'through pipes 3| and 32 to distillation column 5| to recover the butadiene. The vapors from the settling tank 30'contain acetaldehyde, butadiene in 5. anamount or about 20%,diethy1 ether... ethanol. and mono-olefines and saturated hydrocarbon gaseseimtheaamount' or. about 1.0 and. they pass through a pipe-.33 toacompressor 34 where they are .compressedito about 55p: s. i-..

The-compressed vapors and gasespass. through a pipe'SSY-toacondenser'36, where they are cooled.

to; a temperature; of. about; 238- C. Part of the vapors:condensev under theseconditions and the condensate and unicon-denscdv vapors and. gases, are introduced under pressure through pipe 31 to the-base ofascrubbing tower 38, having about 4n. trays- Thefirst. condensate from the acetaldehy'sleaproducing; reaction: is: withdrawn from. tank llrxthrousha pipe-3.9 and-pumped by a. pum -4. through a pipe: ll]; to the top :of; tower 3:8,. This condensate may-contain about. 8 parts. of. acet' aldehyde-,Twparts of ethanol, 13 parts of" water and .2. parts-of acetic acid... This mixture of ethanol and acetaldehyde is a strong solvent for butadiene even in the presence of a small amount of: watenand 'it'is; capable-of: scrubbing completely therbutadiene from the ascending vapors'w-hen employed in. amounts about equal to, or even somewhat less than that. of the'vapors and condensatetentering the baserof the scrubbing. tower at-. -the temperature and pressure specified. The liquid efliuent. from the base. of thetower contains substantially all the'butadiene originally present in-the entering-gases and: it is-withdrawn through pipe 3.2v to distillationcolumni'l for recovery of the butadiene.

'li'hegasesv leaving. the top of tower 3.8 are .approximately saturated. with. the. components of the scrubbing liquid,- principally, acetaldehyde proximately 1.0%. acetaldehyde. 5% .diethylether, 55% -ethanol,.l5.% Water, 10% butadiene and 5% of. other hydrocarbons and. impurities is passed through pump 41 and is'introduced. through pipe Miv under .apressureof 55 to 70 p. s. i. to ahea-t exchanger 4.9, where. it is; heated to about 1-10 0. by-meansrof' a suitable. heating fluid. The feed passes througha .pipe: 50- to a distillation column 5|. at about thefthirtiethtray' thereof. This columnmay' be ofthe. ordinary bubble-cap type with coppertrays; A fifty-five traycolumn possesses suificient trays for the: separation desired with adequateallowan'ceior plate. efficiency. The columnisxheated .lby steam, preferably by me ns -of:.a ealandria through which thecontents of the kettle circulate.

When: the: column: .operates under a pressure oi about 6.5 p.. s. i., theoverhead; :vaporfdistills at about 472C. :and contains approximately 5.0% acetaldehyda; 90% butadiene and. 5.0% butenes and butane. A smallamount of water may also be. present in the overhead vapor. Part of the overhead vapor which is removed through pipe 52 is condensedin a. condenser 53, the condensate being pumped through. a pipe? 54- as reflux: to: the column. The reflux ratio. employed inv the: operation ofythe column may be varied from about 4:1 to 20:1.

The residue. is removed from the kettle '55 through a pipe 56 audit contains acetal'clehyde, di'ethyl ether,. ethanol, water andimpurities. It is tube noted that thescolumn operates with both an: enriching. and. exhausting section, and that the residue is denuded of. buta'diene. The residue passes tothe :recoverydistillation' system through pipe'2'3. I

0f the overhead vapor, the part which is: not

. condensed. and returnedas: reflux passes through dioxide. and carbon monoxide are. discharged from I the system. 'The process just described is the subject to the copending application Serial No. 501,610 of I. L. Murray, J. 'L. Marsh and S. P. Smith, Jr., entitled Process for making butadiene."

However, it is not essential to practice the process of that applicationin order to secure the benefits of the present invention. The condensate from the tank l1 may be withdrawn through by-pass pipe to pipe 23, and be carried directly to the distillation system. The scrubbing liquid employed in column 3 8 may then comprise part or all'oi the make-up ethanol required in the process, which maybe introduced through pipe 46 from ethanol storage tank 41. This make-up ethanol passes to the column for the recovery of butadiene and eventually to the recovery disti1lation system without additional equipment being provided. However, the heat economy secured by feeding the make-up ethanol as part of the reflux required in the operation of the ethanol still would be lost. Alternatively, a separate cycle for scrubbing such butadiene-containing gases may be provided in which the solvent employed as scrubbing liquid isseparately distilled to strip 0d the butadiene; and residue cooled and reused in thescrubbingoperation. y r

A- composite feed from'pipe 32 containing apa valve 5''! and through pipe '58, and enters a scrubber 59 through a pressure reducing valve 60. The scrubber maybe a forty-tray'column which operates at .a pressure. of 35 pounds per square inch'ata-temperatureof 35 C... and it is designed to remove the acetaldehyde. from the butadiene vapor by dissolving the acetalde-hydein water. Butacliene is. agas at this temperature and pressureandit' does not. appreciably condense, whereas at thesame time, acetaldehyde is'readily absorbed in water. .Thewater, introduced at the top of the vcolwnnsfiows .downward and selectively dissolves the acetaldehyde from the ascending vapors. The'vapors-irom the top of'thIe column mayicontain ab out butadiene. and- 5% butenes .and' butane. The bntadiene may be separated from the butenes' and the butane by known .method's,;which are nota :part of. the present invention.

I'he aqueous scrubbing liquid from the bottom of'the scrubbing tower contains a. small amount ofacetaldehyde; and it passes through a pipe 6| to: the recovery distillation system.

The scrubber residues from scrubbers 22, 43, and, and the residue from column 5| are commingl'ed: in pipe .23- to form a composition containing approximately 1.5% acetaldehyde, 5.%-diethyl. ether, 40% ethanol, and 35% Water and 5% Icy-products. This mixture is introduced throughapreheater fizibymeans ofpipe 63 to a distillation column 61. This column may operate at'a pressure-of about 40 p. s. i. gauge'and at a head temperature-"of about 5'7 to 58C. It is heated by steam, preferably by circulating the contentsv of the kettle through an external inclined ca-landria. Amixture. of the. azeotrope of acetail'dehyde and .diethyl ether, together with azeotropes of acetaldehyde and other byproducts, the composition being about 75% acetaldehyde, 20% diethyl ether, and by-products, is withdrawn as vapor through pipe 65, and passes as one of the reactants to the butadiene converte 26. Sufficient overhead Vapor to constitute a reflux ratio of about 3 to 1 is withdrawn through proportioning valve 66 through a pipe 61 toa condenser 68, where it is condensed and returned as reflux to the column 64 through pipe 69. a The residues from column 64, containing principally ethanol and water, the remainder being diethyl ether, acetaldehyde and other by-products pass through a pipe 16 to distillation column H, after passing through a pressure reducing valve 12. This column may operate at a pressure of 20 p. s. i. gauge and a head temperature of 65 to 75 C. It generates an overhead vapor containing acetaldehyde, diethyl ether, ethyl acetate, butyraldehyde, methyl ethyl ketone, and other impurities. This overhead vapor all passes through pipe I3 to condenser 14, where about 1 6 of the condensate is withdrawn through pipe 15 to storage. These by-products may be distilled from time to time to recover their valuable components. The remainder of the condensate passes through pipe 16 to column 1| as reflux. The column is heated by steam, preferably by circulating the contents of the kettle through an external inclined calandria.

In the operation of the acetaldehyde still 64, there is a tendency for by-products to accumulate in the upper third of the column, when the base temperature is sufliciently high, about 120 C., to volatilize all the acetaldehyde from the base of the column. Such icy-products eventually pass from the top of the column and reduce the concentration of acetaldehyde below the desired value. This may be prevented by withdrawing about 2 to 5% of the total down-flow from the column 64, through pipe 11, either in the liquid or vapor phase, and introducing it in the upper third of the by-products distillation column H. The approximate composition of the side stream thus withdrawn may be acetaldehyde, 40%, diethyl ether, 45%, and .by-products, 15%. This process is more fully described in application Serial No. 526,792, filed March 16, 1944, by M. E. Hitchcock and J. A. Field, which is assigned to the same assignee as the present application.

The residue from column H containing mostly ethanol andwater, along with some by-products, is pumped through pipe 18 to distillation column 19 in which ethanol is separated from the water.

This column may operate at a pressure of 50 r p. s. i. gauge and a head temperature of 118 C. It generates an azeotropic mixture of 85% ethanol, water and 5% by-products, which is withdrawn through pipe 80 as reactant material for the acetaldehyde and butadiene converters. The feed to the butadiene converter is withdrawn through pipe 85. About twice as much vapor as is withdrawn through pipe 80 is withdrawn through pipe BI and condensed in condenser 82. The condensate passes to a reflux storage tank 83 .to which is added an amount of ethanol equivalent to that consumed in the process. This mixture is pumped through pipe 84 as reflux fo the column 19. The column is heated by steam, preferably by the direct introduction of steam into the kettle. The aqueous waste is withdrawn from the kettle through a line 84, and before being discarded, it is used as a heating fluid in the various preheaters shown in the system, for

instance, it may be withdrawn through pipe 86 r and employed as heating fluid in heat er:- changer 62; v t

The addition of make-up ethanol as part of the reflux-required in the column used for distillation of the alcohol provides a saving in the heat otherwise required to operatethe still, as described in I. L. Murray Patent No. 2,249,847. Obviously, however, the make-up ethanol may be added in other ways to the cyclic process, as previously pointed out. Modifications of the invention other than as specifically described, may be made without departing from the principle of the invention. The essential features of the invention consist of a cyclic two-step process 'for the production of butadiene from ethanol, them-'- tegration of an acetaldehyde-producing reaction with a butadiene producing reaction, and the provision of a common distillation system for recovering the unconverted products of the two reactions.

We claim: I x

1. A cyclic process for making butadiene which comprises introducing ethanol vapors to a reaction zone, converting a part of such ethanol vapors to acetaldehyde and separating an acetal dehyde-ethanol condensate from the remainder of the reaction products; concurrently introducing ethanol and acetaldehyde vapors to a separate reaction zone, converting a part of the ethanol and acetaldehyde to butadiene and separatingthe butadiene from unconverted ethanol and acetaldehyde; distilling acetaldehyde from a mixture containing such unconverted acetaldehyde and said condensate and passing it to the butadiene-producing reaction zone; distilling ethanol from a mixture of the remainder of said condensate and such unconvertedethanol and returnin said recovered ethanol to at least one of the reactionzones; and introducing additional ethanol to at least one reaction zone.

2. A cylic process for making butadiene which comprises introducing ethanol vapors to a reaction zone, converting a part of such vapors to acetaldehyde and separating an acetaldehydeethanol condensate from .the remainder of the reaction products; concurrently introducing ethanol and acetaldehyde vapors to a separate reaction zone, converting a part of the ethanol and acetaldehyde in the vapor phase to butadiene and separating the butadienefrom unconverted ethanol and acetaldehyde; distilling acetaldehyde vapors from amixturecontaining suchunconverted acetaldehyde andv said condensate and passing such vapors to the butadiene-producing reaction zone; distilling ethanol vapors from a mixture containing such unconverted ethanol and the remainder of said condensate, after expulsion of acetaldehyde, and returning such ethanol vapors to both reaction zones; and introducing make-up ethanol as a reactant to at least one reaction zone.

3. A cyclic process for making butadiene which comprises introducing ethanol vapors to a reaction zone, converting a part of such vapors to acetaldehyde and separating, an acetaldehydeethanol condensate from the remainder of the reaction products; concurrently introducing ethanol and acetaldehyde vapors to a separate reaction zone, coverting a part of the ethanol and acetaldehyde in the vapor phase to butadiene and separating the butadiene from unconverted ethanol and acetaldehyde; combining such unconverted ethanol and acetaldehyde with said condensate to form a mixture containing acetaland introducing make-up ethanol as a' reactant to at least one reaction zone. 7

4. Acyclic process for making butadiene which comprises introducing ethanol vapors to a reaction zone, converting a part of such ethanol to acetaldehyde and separating an acetaldehydeethanol condensate from the remainder of the reaction products; concurrently introducing ethanol and acetaldehyde vapors to a separate reaction zone, converting ethanol and acetaldehyde to butadiene and by-products and separating butadiene from the by-products formed and unconverted ethanol and acetaldehyde; separating at least part of such by-products from unconverted acetaldehyde and ethanol; distilling acetaldehyde vapors from a mixture containing such unconverted acetaldehyde and said condensate and introducing them to the butadiene-producing reaction Zone; distilling ethanol vapors from a mixture containing such unconverted ethanol and the remainder of .said condensate, after expulsion of acetaldehyde, and returning such recovered ethanol to at least one reaction zone; and introducing make-up ethanol to at least one reaction zone.

5. A cyclic process for making butadiene which comp-rises introducing ethanol vapors to a reaction zone, converting a part of such ethanol to acetaldehyde and separating an acetaldehydeethanol condensate from the remainder of the reaction products; concurrently introducing ethanol and acetaldehyde vapors to a separate reaction zone, converting ethanol and acetaldehyde to butadiene and separating butadiene from unconverted ethanol and acetaldehyde; combining such unconverted ethanol and acetaldehyde with said condensate to form, a mixture containing acetaldehyde, ethanoland by-products of the two vapor phase reactions, distilling acetaldehyde vapors from said mixture and introducing them to the butadiene-producing reaction zone; distilling at least part of the Icy-products from the residue from the acetaldehyde distillation; distilling ethanol vapors from the residue of the byproducts distillation and returning such recovered ethanol to at least one of said reaction zones; and introducing make-up ethanol to at least one reaction zone.

6. A cyclic process for making butadiene which comprises introducing ethanol vapors to a reaction zone, dehydrogenating a part of such ethanol to acetaldehyde and separating an acetalde hyde-ethanol condensate from the hydrogen gas produced; concurrently introducing ethanol and acetaldehyde vapors to a separate reaction zone, converting ethanol and acetaldehyde to butadiene and separating butadiene from unconverted ethanol and acetaldehyde, combining such unconverted ethanol and acetaldehyde with said condensate to form a mixture containing acetaldehyde, ethanol and by-productsof the two vapor phasev reactions, distilling acetaldehyde vapors from said mixture and introducing them to the butadiene-producing reaction zone; distilling at least part of the by-products from the residue from the acetaldehyde distillation; distilling ethanol vapors from the residue of the lay-products distillation and returning such recovered ethanol to both of said vapor phase reactions, and introducing make-up ethanol as reflux in said third distillation.

'7. A cyclic process for making butadiene, which comprises introducing ethanol vapors to a, reaction zone, converting a part of such ethanol to acetaldehyde and separating an acetaldehydeethanol condensate from the remainder of the reaction products; converting a, part of ethanol and acetaldehyde vapors to butadiene and other hydrocarbon gases in a separate reaction zone,

condensing the reaction products, and separating a gaseous hydrocarbon mixture containing butadiene from unconverted acetaldehyde and ethanol; bringing such hydrocarbon gases in intimate contact with a scrubbing liquid containing ethanol as the principal constituent to liquefy and dissolve butadiene therein; distilling butadiene from such scrubbing liquid and. recovering a scrubbing liquid residue; distilling acetaldehyde vapors from a mixture containing such unconverted acetaldehyde and said condensate, and passing such vapors to the butadiene reaction zone; distilling ethanol vapors from a mixture containing said scrubbing liquid residue, said unconverted ethanol, and the remainder of said condensate, after expulsion of acetaldehyde, and returning such ethanol vapors to both reaction zones; and introducing make-up ethanol to at least one reaction zone.

.8. A cyclic process for making butadiene, which comprises introducing ethanol vapors to a reaction zone, converting a part of such ethanol to acetaldehyde and separating an acetaldehydeethanol condensate from the remainder of the reaction products; converting a part of ethanol and acetaldehyde vapors to butadiene and other hydrocarbon gases in a separate reaction zone, condensing the reaction products, and separating a, gaseous hydrocarbon mixture containing butadiene from unconverted acetaldehyde and ethanol; bringing such hydrocarbon gases in intimate contact with a scrubbing liquid containing ethanol as the principal constituent to liquefy and dissolve butadiene therein; distilling butadiene from such scrubbing liquid and recovering a scrubbing liquid residue; distilling acetaldehyde vaporsfrom a mixture containing such unconverted acetaldehyde andsaid condensate, and passing such vapors to the butadiene reaction zone; distilling ethanol vapors from a mixture containing said scrubbing liquid residue, said unconverted ethanol, and the remainder of said condensate, after expulsion of acetaldehyde, and returning such ethanol vapors to both reaction zones; and introducing make-up ethanol as said scrubbing liquid.

' IRVIN L. MURRAY.

JAY L. MARSH. SILAS P. SMITH, JR. 

